PDF Publication Title:
Text from PDF Page: 006
III List of Figures VI Fig. 3.4-1 Fig. 3.5-1 Fig. 3.5-2 Fig. 4.1-1 Fig. 4.1-2 Fig. 4.2-1 Fig. 4.2-2 Fig. 4.3-1 Fig. 4.5-1 Fig. 4.5-2 Fig. 4.5-3 Fig. 4.5-4 Fig. 5.1.1-1 Fig. 5.1.2-1 Fig. 5.1.2-2 Fig. 5.2.1-1 Fig. 5.2.2-1 Fig. 5.2.3-1 Fig. 5.2.3-2 Fig. 5.3.1-1 Fig. 5.3.1-2 Fig. 5.3.1-3 Fig. 5.3.1-4 Fig. 5.3.1-5 Fig. 5.3.1-6 Fig. 5.3.1-7 Fig. 5.3.2-1 Heat of adsorption of oxygen and nitrogen evaluated by the Clausius- Clapeyron method; represented by polynomial functions.............................. 31 Mass transfer in adsorbent particle................................................................. 31 Kinetic curves of relative uptake calculated from adsorption isotherm data of synthetic air .................................................................................................... 33 Internal structure of CMS; and general pore size distribution of CMS ......... 35 Adsorbent Shirasagi MSC CT-350 ................................................................ 36 Scheme of the PSA experimental set-up ........................................................ 36 The feed gas preparation and pre-treatment section; the twin-bed PSA plant section; and the product and tail gas analytics section................................... 38 Valves operation scheme in the reference cycle ............................................ 40 Flow rate of process streams during the PSA cycle ....................................... 43 Pressure in adsorbers during the PSA cycle................................................... 43 Normal distribution of the air demand at different product purity levels ...... 45 Simulated distribution of the relative error δsim for the air demand at different product purity levels....................................................................................... 46 PSA performance at different operating temperatures ................................... 48 PSA performance at different adsorption pressures ....................................... 50 Graphical representation of fractional uptake rates of oxygen and nitrogen together with their difference Δ...................................................................... 51 PSA performance at different half-cycle times .............................................. 53 PSA performance at different purge proportionality factor ........................... 56 Experimental and simulated pressure profiles during the blow-down step at product purity of 1000 ppm O2 at different cutting times .............................. 57 PSA performance at different cutting time..................................................... 58 Experimental PSA performance at various controlled flow resistances in the piping system at reference process conditions at product purity level of 1000 ppm O2............................................................................................................ 61 Pressure in the adsorber columns after pressure equalisation at different stem positions of the equalisation valves (Top/Top + Bottom/Bottom) at reference process conditions at product purity level of 1000 ppm O2 ........................... 61 Experimental temperature profiles along the adsorbent fixed-bed at reference process conditions .......................................................................................... 64 Visual demonstration of the oxygen MTZ development with related favourable pressure equalisation strategy ...................................................... 64 Experimental and simulated PSA performance at various controlled flow resistances in the piping system at reference process conditions at product purity level of 1000 ppm O2 ........................................................................... 65 PSA performance at asymmetric pressure equalisation at reference process conditions at product purity level of 1000 ppm O2 ........................................ 67 PSA performance at asymmetric pressure equalisation at reference process conditions at product purity level of 10 ppm O2 ............................................ 68 PSA performance at different N2-receiver volumes....................................... 69PDF Image | Modelling and Simulation of Twin-Bed Pressure Swing Adsorption Plants
PDF Search Title:
Modelling and Simulation of Twin-Bed Pressure Swing Adsorption PlantsOriginal File Name Searched:
dissertation_marcinek.pdfDIY PDF Search: Google It | Yahoo | Bing
CO2 Organic Rankine Cycle Experimenter Platform The supercritical CO2 phase change system is both a heat pump and organic rankine cycle which can be used for those purposes and as a supercritical extractor for advanced subcritical and supercritical extraction technology. Uses include producing nanoparticles, precious metal CO2 extraction, lithium battery recycling, and other applications... More Info
Heat Pumps CO2 ORC Heat Pump System Platform More Info
CONTACT TEL: 608-238-6001 Email: greg@infinityturbine.com (Standard Web Page)